US4740530A - Method for foaming synthetic resin bodies with microwave or high frequency energy - Google Patents

Method for foaming synthetic resin bodies with microwave or high frequency energy Download PDF

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Publication number
US4740530A
US4740530A US07/091,970 US9197087A US4740530A US 4740530 A US4740530 A US 4740530A US 9197087 A US9197087 A US 9197087A US 4740530 A US4740530 A US 4740530A
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United States
Prior art keywords
slab
microwave
foaming
synthetic resin
high frequency
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Expired - Fee Related
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US07/091,970
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English (en)
Inventor
Wolfgang Pip
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Roehm GmbH Darmstadt
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Roehm GmbH Darmstadt
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Assigned to ROHM GMBH, 6100 DARMSTADT reassignment ROHM GMBH, 6100 DARMSTADT ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: PIP, WOLFGANG
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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C35/00Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
    • B29C35/02Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
    • B29C35/08Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/3415Heating or cooling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/56After-treatment of articles, e.g. for altering the shape
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C35/00Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
    • B29C35/02Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
    • B29C35/08Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation
    • B29C35/0805Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation using electromagnetic radiation
    • B29C2035/0855Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould by wave energy or particle radiation using electromagnetic radiation using microwave
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C35/00Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
    • B29C35/02Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
    • B29C35/12Dielectric heating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2033/00Use of polymers of unsaturated acids or derivatives thereof as moulding material
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S521/00Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S521/915Utilizing electrical or wave energy during cell forming process

Definitions

  • the present invention relates to a method for making a rigid foam article by prewarming a rigid heat-foamable synthetic resin until at least a portion of the resin surface is softened and then initiating the foaming process by further heating with microwave or high-frequency radiation.
  • the prewarmed synthetic resin is a copolymer comprising at least 80 percent by weight of units of acrylic acid or methacrylic acid and of acrylonitrile or methacrylonitrile, together with a blowing agent. On heating, acrylimide or methacrylimide groups are formed from the acid and nitrile groups.
  • uniform foam slabs are obtained in a microwave or high-frequency field if a rigid slab of foamable synthetic resin is preheated until at least a portion of its surface is at or above the softening temperature of the resin and the microwave or high-frequency field initiating the foaming process is then allowed to act on the slab until foaming occurs. It is important that a microwave or high-frequency field of an intensity that will induce foaming not be allowed to act on the foamable synthetic resin slab until at least a portion of its surface has been thermally softened. How it is heated is not important so long as this condition is satisfied. If preheating is effected by means of a microwave or high-frequency field, its intensity must be such that foaming will not set in.
  • softening temperature is meant that temperature at which the synthetic resin elastically expands under the foaming pressure without fracturing.
  • the temperature at which this condition occurs may be exceeded, but preferably not to the extent that the temperature region of plastic deformability is reached.
  • any heat source with which the softening temperature can be reached at the surface is suitable for the preheating of the foamable synthetic-resin slab.
  • an air oven in which an appropriately heated atmosphere, usually air, will act on the surface of the slab may be employed, or the slab surface may be exposed to heat radiation. Heating by heat transfer from a liquid medium or a hot solid surface is also possible but is usually less convenient.
  • microwave fields or high-frequency fields can be used for preheating, alone or together with the other heat sources mentioned, provided that care is taken that foaming is not prematurely induced in the interior.
  • a field of appropriately low intensity may be used or the field may be allowed to act on the slab only momentarily or intermittently.
  • the microwave or high-frequency field adapted to induce foaming can be cut in. This is preferably done only when the surface of the synthetic resin slab has been heated completely or almost completely to or above the softening temperature. It is not detrimental if foaming has already set in at the surface. Further heating to foaming temperature is faster than with any other heat source acting only externally.
  • Microwave ovens which are suitable for use in the method of the invention are known in the art, where they are employed for drying, for example. They operate with wavelengths ranging from 1 to 50 cm. The most commonly used wavelength is 12.3 cm, which corresponds to 2450 MHz.
  • the radiation or field is produced by a so-called magnetron and is distributed in the microwave oven as uniformly as possible. The more uniform the field, the lower the danger that isolated foaming zones will form that are not associated with a softened surface zone.
  • the power output of the microwave generator will, of course, have to be based on the size of the synthetic resin slab to be foamed and on the foaming temperature required.
  • High frequency generators suitable for use in the method of the invention operate at wavelengths ranging from 1 to 50 meters.
  • a commonly used wavelength is 11 meters, which corresponds to 27.12 MHz.
  • Such generators are employed to heat-seal plastics and to foam wetted polystyrene beads.
  • Kunststoff-Physik im Gespraech (“Discourse on the Physics of Synthetic Resins"), a publication of BASF AG, 1969, p. 179.)
  • a field distribution that is as uniform as possible will be advantageous.
  • a material In order that a material may be heated in a microwave or high-frequency field, it must be capable of absorbing the respective radiation. That will be the case of the material contains a sufficient number of polar structures. Such structures may be a constituent of the polymer molecules which make up the synthetic resin or they may be contained in low molecular weight substances, such as water or formamide, admixed with it. Synthetic resins having polar structures include those which contain carbonyl, carboxyl, hydroxyl, halogen, amino, or carboxylamido groups.
  • synthetic resins containing a copolymer comprising at least 80 percent by weight of units of acrylic acid or methacrylic acid and of acrylonitrile or methacrylonitrile are suitable for use in the method of the inventions.
  • the polymer should comprise at least 20 percent by weight of acrylic acid or methacrylic acid.
  • the ratio by weight of acrylic acid and/or methacrylic acid to acrylonitrile and/or methacrylonitrile is from 3 : 2 to 2 : 3.
  • the copolymer may contain up to 20 percent by weight of other ethylenically unsaturated monomers copolymerizable therewith, for example acrylamide and methacrylamide, styrene, lower alkyl (C 1 -C 4 ) esters of acrylic acid and methacrylic acid, as well as up to 5 percent by weight of crosslinking monomers having 2 or more polymerizable double bonds, such as esters of acrylic acid and methacrylic acid with polyols (e.g. glycol dimethacrylate), divinylbenylene, triallyl cyanurate, and methylene-bis-acrylamide.
  • polyols e.g. glycol dimethacrylate
  • divinylbenylene divinylbenylene
  • triallyl cyanurate methylene-bis-acrylamide
  • metal salts of acrylic acid and methacrylic acid may be present in amounts up to 5 percent by weight, particularly salts of polyvalent metal ions such as Mg 2+ , Zr 4+ , Cr 3+ , Co 2+ , Zn 2+ , Cd 2+ , Bi 3+ , TiO 2+ , and Pb 2+ .
  • These synthetic resins soften at from 140° C. to 150° C. and start to foam from 160° C. to 180° C.
  • a reaction of polymerized units of acrylonitrile or methacrylonitrile and units of acrylic or methacrylic acid takes place to form units of acrylimide or methacrylimide. Foamed plastics based on polymethacrylimide have acquired considerable commercial importance.
  • such resins also comprise from 2 to 15 percent, preferably 2 to 10 percent, by weight of a blowing agent which on being heated yields a gas or vapor.
  • a blowing agent which on being heated yields a gas or vapor.
  • Formamide, monomethyl formamide, urea, water, and lower aliphatic alcohols are illustrative of such blowing agents, which are well known in the art.
  • Slabs of such a synthetic resin having a thickness of from 1 to 4 cm, for example, are best heated in a circulating air oven at 170° C. to 200° C. until the surface softens and are then exposed to a microwave field. Preheating usually takes from about 5 to 30 minutes, while the microwave treatment requires somewhat less time. By contrast, when foaming is effected by the use of hot air alone, a foaming time of about 2 hours is required.
  • a slab measuring 70 ⁇ 70 ⁇ 23 mm of a rigid foamable synthetic resin having a softening temperature of 160° C. and containing a copolymer of methacrylic acid and methacrylonitrile in a molar ratio of 3:2 together with 8 percent, by weight of the polymer, of a blowing agent mixture of formamide and tert.-butanol was preheated in a hot air oven to an approximately uniform surface temperature of 160° C. within 30 minutes and then treated for 6 minutes with a microwave field whose power was controlled through an operating cycle of 10 seconds of radiation followed by a 50-second pause.
  • a foam slab naming a density of 38 kg/m 3 was so obtained.
  • the microwave oven employed (Sharp Model R 8000 E) had a power consumption of 1.4 kw in the hot air section and of 1.3 kw in the microwave section, with a power output of 650 watts with a 2-liter water load, and had been retrofitted to permit simultaneous microwave and hot air operation. This made it possible to carry out the entire foaming operation in the same unit using only hot air during the preheating time and then cutting in microwave heating for foaming.
  • a slab measuring 120 ⁇ 120 ⁇ 23 mm of a rigid foamable synthetic resin having a softening temperature of 180° C. and containing a weakly crosslinked copolymer of methacrylonitrile and methacrylic acid in the aforementioned molar proportions and 10 percent, by weight of the polymer, of a blowing agent mixture of formamide and tert-butanol was preheated for 30 minutes in a hot air oven to an approximately uniform surface temperature of 180° C.
  • the preheated slab was placed between the electrodes if a high frequency furnace (Model HGV 4001 of the firm Herfurth GmbH) having a useful output of 4 kw at a frequency of 27.12 MHz.
  • the electrodes measured 400 ⁇ 400 mm.
  • a monomer mixture comprising:
  • the prewarmed piece was foamed in 5-7 minutes in a high frequency field as in Example 2, during which 50 percent of maximum output was intermittently applied.

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  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Toxicology (AREA)
  • Physics & Mathematics (AREA)
  • Oral & Maxillofacial Surgery (AREA)
  • Thermal Sciences (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Molding Of Porous Articles (AREA)
US07/091,970 1986-09-11 1987-09-02 Method for foaming synthetic resin bodies with microwave or high frequency energy Expired - Fee Related US4740530A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19863630930 DE3630930A1 (de) 1986-09-11 1986-09-11 Verfahren zur herstellung eines hartschaumstoffes mittels eines mikrowellen- oder hochfrequenzfeldes
DE3630930 1986-09-11

Publications (1)

Publication Number Publication Date
US4740530A true US4740530A (en) 1988-04-26

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Country Status (5)

Country Link
US (1) US4740530A (de)
EP (1) EP0259706B1 (de)
JP (1) JPS6374629A (de)
DE (2) DE3630930A1 (de)
ES (1) ES2016601B3 (de)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4840758A (en) * 1988-09-09 1989-06-20 Phillips Petroleum Company Methods of preparing molded thermoplastic articles wherein radio frequency energy is utilized to heat the thermoplastic material
US4990539A (en) * 1988-12-16 1991-02-05 Basf Aktiengesellschaft Preparation of styrene polymer foam particles
EP0978601A1 (de) * 1998-08-05 2000-02-09 Exploitatiemaatschappij Merode B.V. Verfahren und Vorrichtung zur Herstellung eines isolierenden Elementes und damit hergestellter Elemente
NL1009885C2 (nl) * 1998-08-18 2000-02-21 Exploitatiemaatschappij Merode Werkwijze en inrichting voor het vervaardigen van een isolatie-element, aldus verkregen isolatie-element en dakconstructie voorzien van één of meer isolatie-elementen.
US20040101674A1 (en) * 2002-11-06 2004-05-27 Leslie Ross Composite sheet material
EP1332030A4 (de) * 2000-08-14 2009-02-11 Novamont Spa Verfahren zum herstellen biologisch abbaubarer schaumprodukte
KR100943399B1 (ko) * 2001-08-29 2010-02-22 에보니크 룀 게엠베하 폴리메타크릴이미드 발포체의 제조방법 및 당해 방법으로 수득 가능한 폴리메타크릴이미드의 발포 판 또는 시이트
CN103524968A (zh) * 2013-10-23 2014-01-22 江苏兆鋆新材料科技有限公司 一种石墨烯增强聚甲基丙烯酰亚胺泡沫材料的制备方法
CN106079219A (zh) * 2016-06-08 2016-11-09 惠州景华包装制品有限公司 一种eps泡沫包装箱生产工艺
CN106079217A (zh) * 2016-06-08 2016-11-09 惠州景华包装制品有限公司 一种eps红外线预发泡工艺
CN106432592A (zh) * 2016-09-19 2017-02-22 浙江中科恒泰新材料科技有限公司 一种提高聚甲基丙烯酰亚胺泡沫加工收率的制备方法
CN108084324A (zh) * 2017-12-27 2018-05-29 浙江中科恒泰新材料科技有限公司 一种高强度异型聚(甲基)丙烯酰亚胺泡沫的制备方法
US10919198B2 (en) 2015-10-22 2021-02-16 Evonik Operations Gmbh Production of complex hollow foam or sandwich structures by means of a mold core
CN113286686A (zh) * 2019-01-16 2021-08-20 赢创运营有限公司 制备泡沫材料的新发泡方法
CN113302031A (zh) * 2019-01-16 2021-08-24 赢创运营有限公司 通过使用微波使含有发泡剂的聚合物发泡

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US5242634A (en) * 1991-08-06 1993-09-07 Sanwa Kako Company Limited Method of producing open-cell foams of cross-linked polyolefins
DE19639491C2 (de) * 1996-09-26 1999-11-11 Fraunhofer Ges Forschung Verfahren zur Vergrößerung der Oberfläche von Partikeln
DE102011085026A1 (de) 2011-10-21 2013-04-25 Evonik Röhm Gmbh Verfahren zur Herstellung von Korngrenzenhaftung von expandierten Copolymeren auf Basis von Methacryl- und Acrylverbindungen und Anhaftung diverser Deckschichten auf dem Schaumkern
DE102013002519B4 (de) 2013-02-13 2016-08-18 Adidas Ag Herstellungsverfahren für Dämpfungselemente für Sportbekleidung
DE102013205963A1 (de) 2013-04-04 2014-10-09 Evonik Industries Ag Verfahren zur kontinuierlichen PMI-Schaumfertigung
DE102013225132A1 (de) 2013-12-06 2015-06-11 Evonik Industries Ag Vorschäumung von Poly(meth)acrylimid-Partikeln für das anschließende Formschäumen in geschlossenen Werkzeugen
DE102014209425A1 (de) 2014-05-19 2015-11-19 Evonik Röhm Gmbh Formschäumen von Poly(meth)acrylimid-Partikeln in geschlossenen Werkzeugen zur Herstellung von Hartschaumkernen
DE102014009338A1 (de) 2014-06-27 2015-12-31 Evonik Röhm Gmbh Druckabhängiges Formschäumen von Poly(meth)acrylimid-Partikeln in geschlossenen Werkzeugen zur Herstellung von Hartschaumstoffkernen
DE102015202013B4 (de) 2015-02-05 2019-05-09 Adidas Ag Verfahren zur Herstellung eines Kunststoffformteils, Kunststoffformteil und Schuh
DE102016209044B4 (de) 2016-05-24 2019-08-29 Adidas Ag Sohlenform zum Herstellen einer Sohle und Anordnung einer Vielzahl von Sohlenformen
DE102016209046B4 (de) 2016-05-24 2019-08-08 Adidas Ag Verfahren zur herstellung einer schuhsohle, schuhsohle, schuh und vorgefertigte tpu-gegenstände
DE102016209045B4 (de) 2016-05-24 2022-05-25 Adidas Ag Verfahren und vorrichtung zum automatischen herstellen von schuhsohlen, sohlen und schuhe
DE102016223980B4 (de) 2016-12-01 2022-09-22 Adidas Ag Verfahren zur Herstellung eines Kunststoffformteils
DE102017205830B4 (de) 2017-04-05 2020-09-24 Adidas Ag Verfahren für die Nachbehandlung einer Vielzahl einzelner expandierter Partikel für die Herstellung mindestens eines Teils eines gegossenen Sportartikels, Sportartikel und Sportschuh
CN107325320B (zh) * 2017-07-21 2020-03-24 中国工程物理研究院激光聚变研究中心 避免聚苯乙烯类空心微球干燥过程开裂的方法
WO2026041546A1 (en) 2024-08-21 2026-02-26 Evonik Operations Gmbh Variothermal sintering

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US3627711A (en) * 1968-12-27 1971-12-14 Roehm & Haas Gmbh Foamable synthetic resin compositions
GB2134845A (en) * 1983-02-12 1984-08-22 Roehm Gmbh Process for producing composite form body

Cited By (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4840758A (en) * 1988-09-09 1989-06-20 Phillips Petroleum Company Methods of preparing molded thermoplastic articles wherein radio frequency energy is utilized to heat the thermoplastic material
US4990539A (en) * 1988-12-16 1991-02-05 Basf Aktiengesellschaft Preparation of styrene polymer foam particles
EP0978601A1 (de) * 1998-08-05 2000-02-09 Exploitatiemaatschappij Merode B.V. Verfahren und Vorrichtung zur Herstellung eines isolierenden Elementes und damit hergestellter Elemente
NL1009885C2 (nl) * 1998-08-18 2000-02-21 Exploitatiemaatschappij Merode Werkwijze en inrichting voor het vervaardigen van een isolatie-element, aldus verkregen isolatie-element en dakconstructie voorzien van één of meer isolatie-elementen.
EP1332030A4 (de) * 2000-08-14 2009-02-11 Novamont Spa Verfahren zum herstellen biologisch abbaubarer schaumprodukte
KR100943399B1 (ko) * 2001-08-29 2010-02-22 에보니크 룀 게엠베하 폴리메타크릴이미드 발포체의 제조방법 및 당해 방법으로 수득 가능한 폴리메타크릴이미드의 발포 판 또는 시이트
US20040101674A1 (en) * 2002-11-06 2004-05-27 Leslie Ross Composite sheet material
US7208223B2 (en) * 2002-11-06 2007-04-24 Premium Aircraft Interiors Uk Limited Composite sheet material
CN103524968A (zh) * 2013-10-23 2014-01-22 江苏兆鋆新材料科技有限公司 一种石墨烯增强聚甲基丙烯酰亚胺泡沫材料的制备方法
US10919198B2 (en) 2015-10-22 2021-02-16 Evonik Operations Gmbh Production of complex hollow foam or sandwich structures by means of a mold core
CN106079217A (zh) * 2016-06-08 2016-11-09 惠州景华包装制品有限公司 一种eps红外线预发泡工艺
CN106079219A (zh) * 2016-06-08 2016-11-09 惠州景华包装制品有限公司 一种eps泡沫包装箱生产工艺
CN106432592A (zh) * 2016-09-19 2017-02-22 浙江中科恒泰新材料科技有限公司 一种提高聚甲基丙烯酰亚胺泡沫加工收率的制备方法
CN106432592B (zh) * 2016-09-19 2018-07-17 浙江中科恒泰新材料科技有限公司 一种提高聚甲基丙烯酰亚胺泡沫加工收率的制备方法
CN108084324A (zh) * 2017-12-27 2018-05-29 浙江中科恒泰新材料科技有限公司 一种高强度异型聚(甲基)丙烯酰亚胺泡沫的制备方法
CN108084324B (zh) * 2017-12-27 2020-11-10 浙江中科恒泰新材料科技有限公司 一种高强度异型聚(甲基)丙烯酰亚胺泡沫的制备方法
CN113286686A (zh) * 2019-01-16 2021-08-20 赢创运营有限公司 制备泡沫材料的新发泡方法
CN113302031A (zh) * 2019-01-16 2021-08-24 赢创运营有限公司 通过使用微波使含有发泡剂的聚合物发泡
JP2022518454A (ja) * 2019-01-16 2022-03-15 エボニック オペレーションズ ゲーエムベーハー マイクロ波の使用による発泡剤含有ポリマーの発泡
JP2022518706A (ja) * 2019-01-16 2022-03-16 エボニック オペレーションズ ゲーエムベーハー 発泡材料を製造するための新規の発泡法
US11904514B2 (en) 2019-01-16 2024-02-20 Evonik Operations Gmbh Foaming process for production of foam materials
US12233582B2 (en) 2019-01-16 2025-02-25 Evonik Operations Gmbh Foaming of blowing agent containing polymers through the use of microwaves

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EP0259706A2 (de) 1988-03-16
ES2016601B3 (es) 1990-11-16
EP0259706B1 (de) 1990-04-18
DE3630930A1 (de) 1988-03-24
DE3762324D1 (de) 1990-05-23
JPS6374629A (ja) 1988-04-05
EP0259706A3 (en) 1988-08-03

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